21 European Symposium on Computer Aided Process Engineering by Pistikopoulos E. N. (EDT)/ Georgiadis Michael C. (EDT)/

By Pistikopoulos E. N. (EDT)/ Georgiadis Michael C. (EDT)/ Kokossis Antonis C. (EDT)

The eu Symposium on desktop Aided strategy Engineering (ESCAPE) sequence offers the most recent concepts and achievements of major pros from the economic and educational groups. The get away sequence serves as a discussion board for engineers, scientists, researchers, managers and scholars to provide and talk about development being made within the sector of laptop aided technique engineering (CAPE). eu industries huge and small are bringing suggestions into our lives, no matter if within the kind of new applied sciences to deal with environmental difficulties, new items to make our houses more well-off and effort effective or new remedies to enhance the wellbeing and fitness and health of ecu voters. additionally, the eu must adopt learn and technological projects in line with humanity's "Grand Challenges," defined within the assertion of Lund, particularly, worldwide Warming, Tightening provides of strength, Water and foodstuff, ageing Societies, Public wellbeing and fitness, Pandemics and safety. therefore, the Technical topic of break out 21 should be "Process structures methods for Addressing Grand demanding situations in power, atmosphere, future health, Bioprocessing & Nanotechnologies."

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1-2) the transport of one droplet size fraction is considered, while the micro scale (Eqs. 3-14) describes the evaporation of a single droplet and the required properties are calculated on the nano scale with respect to temperature and composition. Figure 2 shows the linking scheme of the different models together with the data-flow and sketches of the modelled system on the different scales. The macro A new modelling tool for multi-scale model development and evaluation 19 scale models are solved sequentially.

C. C. V. All rights reserved. Detailed Mathematical Modelling of Liquid-Liquid Extraction Columns Moutasem JARADAT1, 3, Menwer ATTARAKIH 2,3 and Hans-Jörg BART1,3 1 Chair of Separation Science and Technology, TU Kaiserslautern, POB 3049, 67653 Kaiserslautern, Germany 2 Faculty of Eng. , Chem. Eng. , Al-Balqa Applied University, POB 15008, 11134 Amman, Jordan 3 Centre of Mathematical and Computational Modelling, TU Kaiserslautern, Germany Abstract A comprehensive bivariate population balance model for the dynamic and steady state simulation of extraction columns is developed.

8), (9) and (10): N iV, j N iL, j (8) N iL, j kl a(Ci*, j  Ci , j ) (9) N iV, j k g a( yi , j  yi*, j ) (10) where, kl, kg are respectively liquid and vapor side mass transfer coefficients (kg/s/m2), a is the interfacial area (m2) and C*i,j, y*i,j are the liquid and vapor side equilibrium concentration of component i, respectively. 3. Results and discussions A reactive distillation model is developed to describe a kinetically controlled reactive distillation process. This model can be also used to simulate a multi-product reactive distillation column.

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